Ahmadun Fakhru'L-Razi
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Research Subjects
Research Interests
Ahmadun Fakhru'L-Razi has a total of 189 co-authors. Here are the top co-authors by number of shared publications:
- Zahangir Alam
Department of Chemical Engineering and Sustainability, Kulliyyah of Engineering, IIUM
16 shared publications - Abul Hossain Molla
Department of Environmental Science, Bangabandhu Sheikh Mujibur Rahman Agricultural University, Gazipur, Bangladesh
13 shared publications - Dayang Radiah Awang Biak
Department of Chemical and Environmental Engineering, Faculty of Engineering, Universiti Putra Malaysia, Serdang, Malaysia
11 shared publications - Zurina Zainal Abidin
Department of Chemical and Environmental Engineering, Faculty of Engineering, Universiti Putra Malaysia, Serdang, Malaysia
10 shared publications - Luqman Chuah Abdullah
Department of Chemical and Environmental Engineering, Faculty of Engineering, University Putra Malaysia, Serdang, Malaysia
9 shared publications - Alireza Pendashteh
Department of Chemical Engineering, University of Guilan, Rasht, Iran
8 shared publications
Latest Publications
- 1 January 2020
- Published by Elsevier in Safety Science
- Vol. 121, 619-631
Consequences of the 2004 Indian Ocean Tsunami in Malaysia
- 1 January 2020
- Published by Elsevier in Safety Science
- Vol. 121, 619-631
Consequences of the 2004 Indian Ocean Tsunami in Malaysia
- 1 November 2018
- Published by Elsevier in Process Safety and Environmental Protection
- Vol. 120, 128-135
Liquid state bioconversion continuous bioreactor of sewage sludge treatment: Determination and evaluation of mixed fungi growth kinetics
- 1 November 2018
- Published by Elsevier in Process Safety and Environmental Protection
- Vol. 120, 128-135
Liquid state bioconversion continuous bioreactor of sewage sludge treatment: Determination and evaluation of mixed fungi growth kinetics
- 15 January 2018
- Published by Taylor & Francis in Chemical Engineering Communications
- Vol. 205 (3) , 387-401
Biological treatment of high salinity produced water by microbial consortia in a batch stirred tank reactor: Modelling and kinetics study
This study was performed to evaluate the potential of acclimated halophilic microorganisms, commercial microorganisms, and microorganisms from polluted soil to degrade crude oil in high salinity oily wastewater (synthetic produced water) at different salt concentrations ranging from zero to 250,000 mg L−1 of total dissolved solids (TDS). The highest degradation of crude oil (>60%) was found for acclimated halophilic microorganisms at TDS of 35,000 mg L−1. An increase in the TDS concentrations above 145,000 mg L−1 leads to a significant decrease in the growth of microorganisms. The results showed that efficiency of the commercial microorganisms was less than the acclimated halophilic microorganisms. The oil biodegradation followed substrate inhibition kinetics and the specific growth rate were fitted to the Haldane model. The biokinetic constants for the saline oily water at TDS of 35,000 mg L−1, i.e., Y, Ks, µmax, and 1/Ki, were 0.21 mg MLSS/mg crude oil, 0.27 mg L−1, 0.019 h−1, and 0.002 mg L−1, respectively.
- 15 January 2018
- Published by Taylor & Francis in Chemical Engineering Communications
- Vol. 205 (3) , 387-401
Biological treatment of high salinity produced water by microbial consortia in a batch stirred tank reactor: Modelling and kinetics study
This study was performed to evaluate the potential of acclimated halophilic microorganisms, commercial microorganisms, and microorganisms from polluted soil to degrade crude oil in high salinity oily wastewater (synthetic produced water) at different salt concentrations ranging from zero to 250,000 mg L−1 of total dissolved solids (TDS). The highest degradation of crude oil (>60%) was found for acclimated halophilic microorganisms at TDS of 35,000 mg L−1. An increase in the TDS concentrations above 145,000 mg L−1 leads to a significant decrease in the growth of microorganisms. The results showed that efficiency of the commercial microorganisms was less than the acclimated halophilic microorganisms. The oil biodegradation followed substrate inhibition kinetics and the specific growth rate were fitted to the Haldane model. The biokinetic constants for the saline oily water at TDS of 35,000 mg L−1, i.e., Y, Ks, µmax, and 1/Ki, were 0.21 mg MLSS/mg crude oil, 0.27 mg L−1, 0.019 h−1, and 0.002 mg L−1, respectively.
- 31 July 2017
- Published by Penerbit Universiti Kebangsaan Malaysia (UKM Press) in Sains Malaysiana
- Vol. 46 (7) , 1017-1024
Thermal Stability and Conductivity of Carbon Nanotube Nanofluid using Xanthan Gum as Surfactant
- 31 July 2017
- Published by Penerbit Universiti Kebangsaan Malaysia (UKM Press) in Sains Malaysiana
- Vol. 46 (7) , 1017-1024
Thermal Stability and Conductivity of Carbon Nanotube Nanofluid using Xanthan Gum as Surfactant
- 1 February 2017
- Published by Elsevier in Applied Clay Science
- Vol. 136, 152-157
Novel kaolinite based coolant for hyperthermal pyrotechnic aerosol cooling
- 1 February 2017
- Published by Elsevier in Applied Clay Science
- Vol. 136, 152-157
Novel kaolinite based coolant for hyperthermal pyrotechnic aerosol cooling
- Top Cited Papers
- 1 October 2016
- Published by Elsevier in Separation and Purification Technology
- Vol. 170, 377-407
Demulsification techniques of water-in-oil and oil-in-water emulsions in petroleum industry
- 1 October 2016
- Published by Elsevier in Separation and Purification Technology
- Vol. 170, 377-407
Top Cited PapersDemulsification techniques of water-in-oil and oil-in-water emulsions in petroleum industry
- 1 July 2016
- Published by Elsevier in International Journal of Hydrogen Energy
- Vol. 41 (28) , 11960-11964
Bio-hydrogen production from palm oil mill effluent (POME): A preliminary study
- 1 July 2016
- Published by Elsevier in International Journal of Hydrogen Energy
- Vol. 41 (28) , 11960-11964
Bio-hydrogen production from palm oil mill effluent (POME): A preliminary study
- Open Access
- 1 September 2015
- Published by FapUNIFESP (SciELO) in Brazilian Journal of Chemical Engineering
- Vol. 32 (3) , 707-724
HOT AEROSOL FIRE EXTINGUISHING AGENTS AND THE ASSOCIATED TECHNOLOGIES: A REVIEW
Since the phase out of Halon extinguishers in the 1980s, hot aerosol fire suppression technology has gained much attention. Unlike traditional inert gas, foam, water mist and Halon fire suppression agents, hot aerosol fire extinguishing agents do not need to be driven out by pressurized gases and can extinguish class A, B, C, D and K fires at 30 to 200 g/m3. Generally, hot aerosol fire extinguishing technology has developed from a generation I oil tank suppression system to a generation III strontium salt based S-type system. S-type hot aerosol fire extinguishing technology greatly solves the corrosion problem of electrical devices and electronics compared to potassium salt based generation I & II hot aerosol fire extinguishing technology. As substitutes for Halon agents, the ODP and GWP values of hot fire extinguishing aerosols are nearly zero, but those fine aerosol particles can cause adverse health effects once inhaled by human. As for configurations of hot aerosol fire extinguishing devices, fixed or portable cylindrical canisters are the most common among generation II & III hot aerosol fire extinguishers across the world, while generation I hot aerosol fire suppression systems are integrated with the oil tank as a whole. Some countries like the U.S., Australia, Russia and China, etc. have already developed standards for manufacturing and quality control of hot aerosol fire extinguishing agents and norms for hot aerosol fire extinguishing system design under different fire protection scenarios. Coolants in hot aerosol fire suppression systems, which are responsible for reducing hot aerosol temperature to avoid secondary fire risk are reviewed for the first time. Cooling effects are generally achieved through vaporization and endothermic chemical decomposition of coolants. Finally, this review discussed areas applying generation I, II or III hot aerosol fire suppression technologies. The generation III hot aerosol fire extinguishing system is most applicable, especially in areas involving delicate electrical and electronic equipments. Nonetheless, developing a much cleaner, non-corrosive and highly efficient hot aerosol fire suppression system is still needed.
- 1 September 2015
- Published by FapUNIFESP (SciELO) in Brazilian Journal of Chemical Engineering
- Vol. 32 (3) , 707-724
Open AccessHOT AEROSOL FIRE EXTINGUISHING AGENTS AND THE ASSOCIATED TECHNOLOGIES: A REVIEW
Since the phase out of Halon extinguishers in the 1980s, hot aerosol fire suppression technology has gained much attention. Unlike traditional inert gas, foam, water mist and Halon fire suppression agents, hot aerosol fire extinguishing agents do not need to be driven out by pressurized gases and can extinguish class A, B, C, D and K fires at 30 to 200 g/m3. Generally, hot aerosol fire extinguishing technology has developed from a generation I oil tank suppression system to a generation III strontium salt based S-type system. S-type hot aerosol fire extinguishing technology greatly solves the corrosion problem of electrical devices and electronics compared to potassium salt based generation I & II hot aerosol fire extinguishing technology. As substitutes for Halon agents, the ODP and GWP values of hot fire extinguishing aerosols are nearly zero, but those fine aerosol particles can cause adverse health effects once inhaled by human. As for configurations of hot aerosol fire extinguishing devices, fixed or portable cylindrical canisters are the most common among generation II & III hot aerosol fire extinguishers across the world, while generation I hot aerosol fire suppression systems are integrated with the oil tank as a whole. Some countries like the U.S., Australia, Russia and China, etc. have already developed standards for manufacturing and quality control of hot aerosol fire extinguishing agents and norms for hot aerosol fire extinguishing system design under different fire protection scenarios. Coolants in hot aerosol fire suppression systems, which are responsible for reducing hot aerosol temperature to avoid secondary fire risk are reviewed for the first time. Cooling effects are generally achieved through vaporization and endothermic chemical decomposition of coolants. Finally, this review discussed areas applying generation I, II or III hot aerosol fire suppression technologies. The generation III hot aerosol fire extinguishing system is most applicable, especially in areas involving delicate electrical and electronic equipments. Nonetheless, developing a much cleaner, non-corrosive and highly efficient hot aerosol fire suppression system is still needed.
- 1 July 2015
- Published by Taylor & Francis in Environmental Technology
- Vol. 37 (1) , 1-15
Optimization of process parameters for pilot-scale liquid-state bioconversion of sewage sludge by mixed fungal inoculation
Liquid-state bioconversion (LSB) technique has great potential for application in bioremediation of sewage sludge. The purpose of this study is to determine the optimum level of LSB process of sewage sludge treatment by mixed fungal (Aspergillus niger and Penicillium corylophilum) inoculation in a pilot-scale bioreactor. The optimization of process factors was investigated using response surface methodology based on Box–Behnken design considering hydraulic retention time (HRT) and substrate influent concentration (S0) on nine responses for optimizing and fitted to the regression model. The optimum region was successfully depicted by optimized conditions, which was identified as the best fit for convenient multiple responses. The results from process verification were in close agreement with those obtained through predictions. Considering five runs of different conditions of HRT (low, medium and high 3.62, 6.13 and 8.27 days, respectively) with the range of S0 value (the highest 12.56 and the lowest 7.85 g L−1), it was monitored as the lower HRT was considered as the best option because it required minimum days of treatment than the others with influent concentration around 10 g L−1. Therefore, optimum process factors of 3.62 days for HRT and 10.12 g L−1 for S0 were identified as the best fit for LSB process and its performance was deviated by less than 5% in most of the cases compared to the predicted values. The recorded optimized results address a dynamic development in commercial-scale biological treatment of wastewater for safe and environment-friendly disposal in near future.
- 1 July 2015
- Published by Taylor & Francis in Environmental Technology
- Vol. 37 (1) , 1-15
Optimization of process parameters for pilot-scale liquid-state bioconversion of sewage sludge by mixed fungal inoculation
Liquid-state bioconversion (LSB) technique has great potential for application in bioremediation of sewage sludge. The purpose of this study is to determine the optimum level of LSB process of sewage sludge treatment by mixed fungal (Aspergillus niger and Penicillium corylophilum) inoculation in a pilot-scale bioreactor. The optimization of process factors was investigated using response surface methodology based on Box–Behnken design considering hydraulic retention time (HRT) and substrate influent concentration (S0) on nine responses for optimizing and fitted to the regression model. The optimum region was successfully depicted by optimized conditions, which was identified as the best fit for convenient multiple responses. The results from process verification were in close agreement with those obtained through predictions. Considering five runs of different conditions of HRT (low, medium and high 3.62, 6.13 and 8.27 days, respectively) with the range of S0 value (the highest 12.56 and the lowest 7.85 g L−1), it was monitored as the lower HRT was considered as the best option because it required minimum days of treatment than the others with influent concentration around 10 g L−1. Therefore, optimum process factors of 3.62 days for HRT and 10.12 g L−1 for S0 were identified as the best fit for LSB process and its performance was deviated by less than 5% in most of the cases compared to the predicted values. The recorded optimized results address a dynamic development in commercial-scale biological treatment of wastewater for safe and environment-friendly disposal in near future.
- 12 September 2014
- Published by Trans Tech Publications, Ltd. in Applied Mechanics and Materials
- Vol. 625, 864-869
Methylene Blue Removal from Aqueous Solution by Hylocereus undatus (Dragon Fruit) Foliage
Dragon fruit foliage in its natural form was applied for decolorization of methyleneblue,a cationic dye from aqueous solution. The effects of major parameters like initial dye concentration, pH, adsorbent dose, temperature and contact time were investigated in batch experimental set-up. The optimum values for removal of methylene blue were identified to be pH 9.0 with 30 hours contact time using 1.2 g L−1biosorbent dosage at 250mg L−1 initial dye concentration. The present results suggested that foliage of dragon fruit can be a potential agricultural byproduct to be used as an environmental friendly and low cost biosorbent.
- 12 September 2014
- Published by Trans Tech Publications, Ltd. in Applied Mechanics and Materials
- Vol. 625, 864-869
Methylene Blue Removal from Aqueous Solution by Hylocereus undatus (Dragon Fruit) Foliage
Dragon fruit foliage in its natural form was applied for decolorization of methyleneblue,a cationic dye from aqueous solution. The effects of major parameters like initial dye concentration, pH, adsorbent dose, temperature and contact time were investigated in batch experimental set-up. The optimum values for removal of methylene blue were identified to be pH 9.0 with 30 hours contact time using 1.2 g L−1biosorbent dosage at 250mg L−1 initial dye concentration. The present results suggested that foliage of dragon fruit can be a potential agricultural byproduct to be used as an environmental friendly and low cost biosorbent.